Note : Les descriptions sont présentées dans la langue officielle dans laquelle elles ont été soumises.
WO 91/00248 ~ T`/ A i 190/002~9
~ ~ ~.'S `.~
TITLE: PROCESS ' .-` ~ ?~ ~r.,~T CF A
- SOLUT I GN
-
BAC~GROUND OF THE lNVEN~
1. Fleld of the Inventlo.s
The present i~ve.n~loi. re_aLe~- -o ~rocess ~or r.educlng
the cyanide content of a s o i ;.i ~ 1 o, .
The use of an alkallne acueous so`~tlon of ~ cyanide salt
for recovery of gold and/or .~llvr~ tai~ieS -,oir~ 3res, taillngs
and wastes has heen we~ lOW.-. an ~o~.lme~.ed ~cr a iong
period. While th.~s i~rOCeSr, i.5 i~e,.. ~-.O~'S -~a ;~de,y used for
such preclous meta:~ ..eco;~ery ~ ,so ~o :}~- l;nderstood that
the waste water streams 'rom Sl~c: ~-ocesseC. conta.ln cyanide
in solution which could he danqe~:-ous ~- allowed to enter the
environment and part;-u ~-~rly s~e --:a~ ss,~pi-
For this reasos, ~aste a~sliec~ oees- s~;ear,~ rom gold
treatment plants ~s-~s~ lk~l Llne e'v'ai,_S~ aO`. i' lOSS as the
leachant must meet spec~flc cc.~os;~.c~ i.s before they
are discharged intc th~ e~.vl~~ ~r~es~ . ; - ~3-~ i ~lar, the
~0 total cyanide and free -~a,.;se -o..cce~~-a~~o~.~ s. ~e below
the maximum limits seL by lc,cai. s~a~e a.d LederaL licensing
authorities.
Similar requirernent, ~re .:x~osei^. o,- ~he effluent
discharged from cyan~Lde p~oduc- o. ~ian~s a~.d ,rom other
industrial processes some of ~.~ c~. p~o~ce ;~aste water
~.-. streams containing other specles no.abi~ am~onla ~s well as
- ./r~ cyanlde ions.
2. Discussion of the Prlor Art
A number of processes have been proposed ~o bring about
the chemical breakdown o'- the -otal and free cyanide
components of typlcai effluen- streams. Some of the
.processes have been patented and several are presently used
- on the commercial scale.
High temperature hydrolys.~c brin~s about the total
destruction of the cyanlde lon, b~ he hlgh ~emperatures and
extended retentlon t~.mes requlred makes thls process
~inefficient in cost terms. Some chemlcal reagents convert
. . '~ ~ .
-
,~ .1 ,, ~ ,,~
WO91/0024x PCrIAU90/00289
2 ~ 8 ~ l
the cyanlde lOS ~r. -~ -yana ~ . many 1.ocalities,
scharge of c~,:.a.=: :.e ;T.~ urtne~ estructlon
of cyanate m~en~ o~ _ostly ln reagent
consumptlon ter,~c ~ ac- requlre a different chemlcal
reagent.
The complexi~y o~: ~ yd~ e ~eat~ ., iS compounded by the
presence of othe~. spe~1eC .a~ s .~s. -. tha interfere wlth the
destructlon mechan.~s~, andjor s~bstantlally lncrease the
capital and operatlng costs One such specles is dlssolved
ammonia. `i"
Treatment of an ~'f1.ien; c~- processlng llquor contalning,
for example, aI ~qulralent oncen~ration of cyanide ions and
dissolved ammonla, by th~ standard cyanlde destruction
methods lS unsatlsfactory ln terms of additlonal reagent
consumptlon, increased capital a..d operatlng costs and/or
incomplete cyanlde destructlo... ?hese methods include the
use of hydrogen peroxlde, ^r.lc.-;ne, chlorine/calciUm
hydroxlde, hypochlorite, or sulph1- dloxide.
The applicants are aware o- example, of a proposal
described in Austra.i.a- ~at.e.. ~ App'icatlor. -13261/81 (PCT
International r~1Dll s ;.o~ ;;O82!00288I 'or removing
cyanide ions tro~ SO~ .= .rI s process provides for
adjustlng the solutlon to a pH o a. ieast about ll and to a
halide conten at .ieas~. equl~a.ent tO the cyanide
concentratlon. ~iec ~ ~.fs~ .. ?er ormed uslna intense
agitatlon of the e ec~ ..y~e ; ~.es.. ~.n depos.tion of solld
carbon on the anod~ e~ .y i~- ~ethods generally require
a readily avallab e source ^.~ cheap eiectrlcity for economic
operation and thls is not aiways a~Tallable in remote areas.
Further, thls proposa ~Aoe~. no~ dea. with any dissolved
ammonia also presen~ ln ,ne .~as~e ~ate~- stream.
Australian Pater.~ Appllca_lon 7053/88 (PCT International
Publication Number WO 88J08408) reiates to a method for
separatlng by aeratlon a omponen~ su h as cyani.de from a
llquid contain~ng ~hL _Or~?Gne; ~ne methcd comprises
passing the llquld tn~ou~i ar arr~ of aeration columns
arranged in stages so that the ~lquid flowlng from one column
WO91/0024~ Pr/AIJ90/00289
~3i~ ,3 ~ ~
ln a flrs~. stage .~5 ~1. ..~le~ ~ ^. ,`0`.~ ,t;-~ams which
are lntroduced lri~c sepa.at-. ,e~ .o;. -~ in ;;; a successlve
second stage. .~o~e~er ~ ~O ess ; - ~lKe~';Se UllsUltable
for use in remote a.^eaC an ~ r ~ re~ e.~y .~eai. hlth
any dlssolved amrior.~ se~ .s~e .~'?. '.P' s~stem.
Australlan Paten A~? ~ e,at~ , ~he
chlorlnatlon of waste ;~ater -oi~aln~na ai~mon~a, cyanide and
phenol. This me~hod ~ ive.-. ad~l.,q a -hlor.~natl.ng compound
to the waste wate m, a ~irs~ ~iessel a~ R '~ ~O ~ I passlng
i0 the waste water ~o a secon~. .esse~ at ~ r tc 8 and
controlling the addlt~.on c~ .ioI^lr.a~ln~ compound in
response to the redo~ pot.entl.al lr. ~,e second ~essei so as to
maintain the redox po-ent.l.ai ~. 6~ vol~ to 750
millivolts. This me~noc re~i..C. ..ose ~o~. O;l-~ o~ redox
potentials and .~s s~e~lf,;:ai.~ ec~.e~i a. waste water
;.containing phenol a~ ;ei; as ai~monla and cyanlde
. "~ contaminants.
SUMMAR~ OF THE INVE~'TIO~
It ls accordlngiy an ob,ec; o~ ,e ~ese.,~. ln~ention to
provide in one embodlment an _mproved process for reduclng
the cyanide content of a so~.ullor containing both cyanide and
dissolved ammonia.
We ha~e no~ fou.~d tha~ ~,he yanide concentratlon of an
effluent or process strea~ ontaln~.ng botn cyanide and
dissolved ammonla can be lowered to a levei acceptable for
discharge by a combinat~.ot-i o-: steps A~cordlngly, the
present invent-ior, ~ro;l~es ..,~ .e e~boclm~n' a process for
reducing the cyanlde oo~te~s ~: 3 SC.'~;~ ;Oi~` O ontainlng ~oth
cyanide i~ons and d~ssoived ammonla, _omprislng the following
- consecutive steps:
(a) adding a haloqenat.~n~ aqe,~ e solutlon while
maintai.nlng ~he p~ o. ~..e SO.ut~.on a. ~reater than 7;
(b) removin~ a~monla '-rom ~ne solu,lon ~y aeratlon;
( c ) acidify1ng tne sol-1tloli to a pH of less than 7;
(d) substantlaily neutralls;ng the solutlon; and
- (e) removing the ammonla ~rom ~he solut~cn by aeratlon.
~'''~'' ''
WO91/0024X T'Cl'/A~90/00289
We have ';o~ir:- ~s~ a~~ f s~.eps 1s effectlVe
ln terms of bo~ aY~ operat1ng _osts and suitable for
use ln remo~e _os"atlons.
In step ~a ~ne ~< rna~ be oetween li and 12 and most
preferably abc~ -e-e--Gr~ rGagent for raislng the
pH in step (al die/ l- s,e, :d~ . so~ : hydroxlde,
In step (c. ~,a.- Dret~ er~ s iess ~,han 5 and most
preferably from 3 to ~.
In step (c.~ t~t- p~ ,r~ substa~tlallv neutrallsed
10 SOlUtlOn ITlay De ~ O..'. ' an~ ::o.~ efe.-ably n ~he range 6 to
7 .
The ammonla r,-,a~ i)t~ ~ei~io~er~ ~ rO~! the solution by aeratlon
in the forrn of di~ St~pp` i`'~ ~e~,oveo or stripped ammonia is
preferably colLe;te_ ln ~ a~,..e aas s~,ruDb~r.g I,ystem.
The halogenatioi. dqe.~ L~ e~a~ ~, a o~.lor~natlon agent.
The chlorlnatlon agen~ c~ ., -,, gent capa~le of generating
andjor llberatln~ -ni.or:.ne i:, aq~eous sclutlon. Chlorlne gas
and agents capable of generating and/or llberating chlorine
gas ln the sois~,on a.-e ~artl_ulariy Dreferred for use as
halogenatlon agents .n accordar.ce wlth .he presen`, invention.
Hypochlorltes s~lch as sodlum hypochlo-lte have been found
suitable for use as chlor,natlon agents ln accordance with
the present lnvention.
Where the ch'orlna.lon ~aer, i~ added ln the form of
gaseous chlorlne .`ne addltlor ~ e ~;~uor may be achieved
by means of a sul~abl~ qa~c spargln~ or bubbling system to
oxidise the cyanlde tO cyanate.
In the process provided hy ~he ~resen~ ~nventlon, cyanide
ls converted by cxioa~,ior. ~:~, s.,e~ ~a .^ cyanate, whlch in
step (c) is hydrolysee' s~ on;a and carbon dloxlde. The
carbon dioxlde ,;~ ~-eaclly removed from ~he reactlon system,
Step (c) may be consldered as an ac di r ' cation and hydrolys1s
step for conver..ng ,ne ~yana.e ior ~rom the substantlally
ammonia free solution produced ir s~ep (b) to produce ammonia
and carbon dloxide.
Steps (d) and (e? nave tr,e effect of re-neutralising the
liquor derived frorr, step ~c) followed by removing the
WO' '00~48 1'CT/AI.i90/00289
; ~ ~ r ~ 8 0
dissol.ved ammonl~ t~ dsaed ~ ^O~YS;S of the
cyanate ion. ~ î tl ~ O ` S -i O`I 1~ J be low in
ammonla and conta~ tt:. `. e i~ y?~"l~e
Eac~ step ma~ ~e ..CI`~-iee `'.' '`' empe~ ure~ close to
amblent temperatu~ 'SiS'-i.L.; . '~ ' ~oe~ t'lOt req~;lre
the use of exotlc ma e,iais .- ~s.-~ o;~ ;.A ,ne use of
complex chemical er,gineerina ~?~-;n..p~es
The present i~ven~ion uses ^se -ffec~lve comblnatior, Of
various known prc~,e~se~, ,o~ o~ s, or L, dny
other combinatlo,~ O~ -e=.;'.~ e:..:~;ed by ~he
present. lnventic~,-. r~ r, .~ .a~ esen; process,
sequentlally lnvc.i.;~ .ep~ ,. . e ~ and ( e). The
process t,hus pro~ldes d uniq.le :~e~ o~ a;;~ u~stantial and
unexpected advantages f:o~- ~-t ea~ ~en~ a~ .?.~ ers
More importantly, r>e~ca~i~-;l. -:-.-- -,:i~a-:.o:-. o. cyanide to
cyanate and the remo;!a:. of a.~ss~ e--. ~mot,~a .?.re ~.arrled out
separately, reagen~ consump~,,.o.. lS m~ini~lsed. This
particularly applies sc step a`,, hhere ~ests show that
complete oxidation of cyar~ -ya,.a~* ;a achieved by
20 addition of typlcally ~ .e^ ~"h,~ ~.oi.chlometric
requirement of the halogena~los ages;'.
Another signlflcant advantage o' ~e p.esent process is
that decompositlon of cyana~ie ~ ~mor,~a a-.~ carbon dioxide
does not require the use of cos~.~; ;-ea~e~ts
.
EXAMPL~.S
The present lnvention lS fur~her des~ribed ln the
following non-llmitlng examples of ii.l~ssrati~e embodlments.
Exam~le 1
Initial laboratory scaie t.es~.~n~ o' ln~iv,dual steps in
the process of the lnventlor. were oarrled out to demonstrate
under controlled condltlons the operatlon of individual
steps,
A. ~xamPles of the Oxldation ~ e~
As the source of ch~.orine, --le ;.aboratory sestwork used as
a chlorlnating agent a solu~lor. of ~;Odium hypochlorite with
an equivalent ~ree chiorlne colren~ oL i~ /L as determined
,~
~09l/On24X PCT/AU90/002X9
cl~ratlo~-. a~.c~ c~ scl.l;t,l.oll
so;.u~ o; ~ p~ o' cyan~de lon (as
~,od.ui~. sya-.~.c~e ~;,;as treated wlth the
abo~e SO.`~_10~ C;.`~;i. --.`.-~ `_:`:.. ,.~,:.- a~ ne cyanide
~oncen~ratlc,n ,;~t j ~ r elec~.rode as a
functlon of the -~s:-ies t`'~ i,' ,,e'-' -'`,S,~.e l'i Test i, shown
ln Table 1, the ~ie~ o~ ;^, L''' . ':e sufLlclent to oxidlse the
amount of cyanlde ~rese~ I.r: the sol~itl,on to cyanate ion, was
0.54 g. The pH va,, .,.:: 9---,.~ y the test.
0
able ~
Test 1: Oxida.lon oI ~yanlde '1000 ppm) to Cyanate wlth
Chlorlne ln the presence ~f ~ onla ;1000 ppm)
Chlor1ne Aàded_yanloe Concentratlon
(gmsj (gms)
0.26 311
0.3g 136
0.50 37
0.52 17
0.5 6
0.~9 0
Test 2 was ca~ e^ ~same ~ay as Test 1 except
that the lnlt1c~' ~,.. ,1. o: .-~ oi~me and conta1ned
2000 ppm of cyani~e ,.oi ;lnC. ~O~ pm 0~ ammonia~
.r'ab_e ~
Test 2: Oxldatio . ~ e ~00~ p~" tc Cyanate with
Chlorlne in the presene* )~ Ar... ^,nia ;2C`00 ppm)
Chlorine Added'yanide Concentration
(gms) (gms)
0.26 547
0.39 241
0.50 64
0.52
0.55 6
0.59 2
B, Examples of the Hyd-GLysls Step
WO ~1/002~8 1~ J90/002X9
r, ~
As a pure sou.ce 01 -yai` `!'~ 3 1 ~/L
potass1um cyanate ~as is~
In Test 3, 2G~o . .o; ;a~s treated
with sufficlent s;l..pn.:..-,- ?.C. -' :- S ;~:~r '~ s'al~ pH 3 0 at
room temperature. ~ -e.^ls~ .,-.o,-:... son-er,~atlon as
hydrolys1s of cyanat~-~ pm~cee~-~ec -~â ~eas~ire s r~ SpP~lf ~.C IOn
electrode. The res.~i~,s are snown in labie 3
Table 3
Test 3: Hydrolysi.s of Cyanate lor ~o A.~mon.a at pH 3.0
Tlme Ammo;~Conversion to
~min)oncentra~io.,~,o Ammonla
(ppm` (%)
1 152 15
340 34
58~ 69
) 60 ,.,034 iO3
20'
!
Test 4 was carrled o~u~ ..- ~.î.- aam* ~a. ~ .es. , except
that the pH was ma,.ntained a pk. ~
Table ~
Test 4: Hydrolys1s o' ~yana-e .cn ~c Ammon~a a~ pH 3.5
Time AmmonlaConverslon to
(min)Concent,.at~.or.to Ammonia
(ppm) (%)
1 124 15
195 20
48~ 48
759 76
':: 105 .~.,027 103
/.:
Exam~le 2
A test run was .a~r.. e~ orepa~ea a~eous solutlo~
containing 2,000 mg~ p~ ; ]. ~-^ a;-a .~ per litre
to simulate a waste process .;~ ea,~ from ar, in~ustrlal process
WO91/00248 ~'r/A~90/00289
contalnlng bot~. Ayanlde lO~S a.~d ~ils~ ed ammon~a.
(a) ~hlorl~.a~lo.i:
~n~ s~ ;. ll a ~ i ~ r~ t O oxldise
ali C~- to C~ ;.. Ti ~ osslble~
It wa De ~ l ev~ , sr.a-, -lse ln redox would
OCCUL at r ~'le ~ s~ s~ et ~ ~ addl -lon point i . e ~
where CN conce.. t~at ~~ ni
The p~j ~in.;n~ ` j-j! '~S`~ iiC~;.Or was held at 11.9-
12.0~
Chlorl-iatlo~ a~ -e~ A.(Ar~-~c ~v the addlt1on of sodium
hypochlorite r~ie -e~u:, t.~ ù~ a~-lsed ln rrable 1 which
shows that '~ ? ~ `~' d '. ~ V ~ 0 5 %
'ra~le 1
'rIMEHYPG A3DE~ R~DO~ pH CN
(mins)(~ Sto ch~ (mv) (ppm)
" - ,16 l1.4 1,210
2 11
22 t 10 11 . 9
- 21 33
24 716
29 44
37 - 46 11.9
38 ~6
47 384
53 67
78 - 92 11.9
79 7 R
g5 105
100
129 - 7& '1.9 18
134 1~0
148 - i_ 11.9
157 4
161 103
174 ~- 5 l2.0
176 lv.
189
191 ~ 8 12.0
192 108
206 + 2G 12.0
(b) Flrst Aeratlon
W09t/0024~ P~r/AIJ90/002R9
The CNO-/NH3 in~ r~ me- ~i` a~-OSr~A '?~- `2 ~r. the
chlorinatlon stec~ ;ass~ ,o~ pacKed column to
remove the bulk ~ o~ er- iea;~ , a weak
NH3/CNO- solut1or,~
~he column usea ~':o~ ';2_' ~: `^ m Lel~gt~ c~ 3~0
mm Class 6 PV~, p,~e aac~ed ~ , . o' : ~eilere~tes A1r
flow was ~roduce~ ...... a~ ,,oi. meas~i~.^ed a~ the
fan outiet using ~ ^-e:-, ,;qucr ~.-low
was visually mon,~c.L^~c .~ me~a.,~;red
1.G by level change ~ e aeac~
L1quor flow wa'-, pl,oiu-eci .~. .-e~ ai ~lmF~ runlllng at
- 2800 rpm.
Ammonia remov,~ t; ,~ 1,
The area speclf~ a e~
~lquor = ~ 55 _m~2sec-i
A.r = ~62 m3m~-im-2
Exit gas assays via drager ~sibes lnd;caLed 450 ppm v/v
NH3.
The drager tube rea~s ~ d -~.e~- baslc specles
(amines) ln the sample gasi, e.~ mc;-io_hioramlne, etc.
.., "
. . .
(c) (d) ~cid HYdrolYsis
The solutlon formec~ e~ s ~ade acidic
to hydrolyse all CNO- tc, N;i,~ o ~owed ~ ea~.s-ic additlon to
raise the pH, converting NH4+ ~ H3
CNO- destructlon was ver~ ~^apid, probably less thar 30
minutes.
;:. The acid and caust;c ~-e~ e~er.;- ~c~- -slS stage were
about 6 kg H2SO4 m-3 for p'~ o s.. 3 and ~ ~g NaOH m~3 to
30. raise pH from 3 to 12 It was ao~ed ~ha some foamlng occurs
when pH falls below 7.
(e) Second Aeratlor.
~ he NH3 lr. ~h~ d . ~ SO ~ ;m ` ~ ` formed lr, the
acid hydrolysls stage was removec ,c the atmosphere 1n a
second aeration
Ammonla removal dur~ S se_cnd aera~lo-~ was 92~ at an
Air:~iquor Ratlo of 4750:i
':~` '`
WO9T/002~8 PC.~`/AU90/00289
rrhe area ~-j?~ L.l~.- ` ai t'~ ,` cnls second aeration
were~ ac~ m-~sec~ î
? 4 ~ 2
The drage~- -',~S'!' .-;'-1;...~., .': ''-~ r '^~ '.';'i--. aga ri used on the exit
gas glvlng ai. In_i~;,a~ .i" ~ ;i3 ~.n tne exlt gas.
Calculatlons bas~ .o~ ilOws and ~ne reductlon
ln the sol~tlo~ .,e~e.,s ~ed~ ~ ~?C ppm v/v NH3 1n the gas
phase. Hence, ~n~ cl~cge. r:~ib~-. a?pedr to gl~e reallstic
figures in th~s S~dge, a.. ..~
The concluslcr, ~n~ a~. ~t ~ rom ti~1s example is
that chlor1natlon of cn,~ al. oe achleved by near
stoichlometric ddci~icn c- r~ ..ne ~ small excess seems
necessary, pOSS ~ iUe~ O'' ,'~ mmor,la at che lower
CN- levels.
Str1pp1ng ol ~;i., ..3~ ne ~i~a.''ne SO~UtlOnS lS very
efficient Wlt,n ~ood - a ` ~ soiut~ons belng obtained.
Chlorinated am;r-les r ..~ w3uid not appear to be a
problem espe- ... ..;.:. ~;..:.;-. - ::.. ~ :.a~~ os,ng control.
Cyanate conve-~sioi. ~,s , t ~ a~eei and c~a~as ~.s not a
problem.
Whlle it has bee~ cnve:merl -c desc.lbe the lnvention
nereir lr. rela..e~.-, ;.., ..-.: . cre~erred e~bodiments, it
is to be app.ec.a~e~1 ;n~ m;, d_r.lel.,s arld arrangements
are also consldere' dS ~.â _~`_ W` ~.1_.. the scope of the
lnventlon. varlolis mod..fl-a~l.ons, alcera~lons, variations
and/or addltlor.s ~c tnt emDo~lmentS and arrangements
descrlbed herel!. a.:- a.`~:c ~.,r.s ~ere~ as l'.a~ ng within the
scope and ambl- Ot the ~resl~r; r.ven~.o.l as deflned by the
claims.
